Method for producing fluorine-containing olefin

Description

[0001] The present invention relates to a method for producing a fluorine-containing olefin which is useful, for example, as a monomer modifying for an ethylene/tetrafluoroethylene copolymer.

BACKGROUND OF THE INVENTION

[0002] Conventional method for producing a fluorine-containing olefin involving a 1,1-dihydro-2-fluorovinyl group generally comprises the following steps: the hydroxyl group of a 1,1-dihydro-2,2-difluoro alcohol (referred to as a "fluoroalcohol" hereinafter) is substituted by a halogen atom; and then the resulting halide is dehalogenated with zinc.

[0003] A method for halogen substitution of a fluoroalcohol has been reported, e.g., in J. Am. Chem. Soc., vol. 75, p. 5978 (1953), in which the fluoroalcohol is tosylated and then reacted with a halide such as sodium iodide. The reaction scheme is indicated below.

[0004] In the above formulae, R_f represents a perfluoroalkyl group or a fluoroalkyl group (same as in the formulae referred hereinafter).

[0005] This method is convenient and useful in laboratory scale production, but has numerous disadvantages, such as (i) expensive reagents (such as p-toluene sulfonic acid chloride and sodium iodide) are used, (ii) in the reaction of the above formula (2), the reaction must be conducted at a high temperature using a high boiling point organic solvent (such as diethylene glycol), (iii) a large amount of waste solvents having a high boiling point must be disposed. Therefore, this method is disadvantageous for the production of industrial scale.

[0006] Another method for halogen substitution of a fluoroalcohol has been reported, e.g., in U.S. Patent 3,038,947, in which the fluoroalcohol is reacted with a thionyl halide in the presence of an amido compound as a catalyst. If the amido compound is not used, the fluoroalcohol cannot be reacted with the thionyl halide. The reaction scheme is indicated below.

[0007] This method is convenient and useful compared to the aforementioned method, but, in view of industrial production, has various disadvantages, such as the use of toxic substance (such as thionyl chloride) and the generation of a large amount of an acidic gas.

[0008] The dehalogenation reaction of the thus obtained halide can be conducted using zinc. The reaction scheme is indicated below.

[0009] This reaction is relatively easy, but, in view of the industrial production, has various disadvantages, such as (i) the reaction rate is extremely low when a chloride is used, (ii) an organic solvent such as methanol or dimethylformamide is generally used in the reaction, and the waste of the organic solvent must be disposed, and (iii) a waste of zinc halide containing non-reacted zinc must be disposed.

[0010] As described above, conventional methods for producing a fluorine-containing olefin have numerous disadvantages when they are practiced industrially.

SUMMARY OF THE INVENTION

[0011] An object of the present invention is to provide a method for producing a fluorine-containing olefin involving a 1,1-dihydro-2-fluorovinyl group which is free from the above prior art problems, can easily be practiced industrially, produces less amounts of wastes, and can be conducted cheaply.

[0012] Other objects and effects of the present invention will be apparent from the following description.

[0013] The present inventors have conducted various investigation for attaining the above objects of the present invention, and have found that a fluorine-containing olefin involving a 1,1-dihydro-2-fluorovinyl group is produced when a fluoroalcohol is contacted with hydrogen gas. The present invention is achieved based on this finding.

[0014] The present invention therefore relates to a method for producing a fluorine-containing olefin represented by formula (I):

        CH₂ = CFR_f   (I)

wherein R_f represents a perfluoroalkyl group or a fluoroalkyl group
   comprising the step of contacting, at a high temperature, hydrogen gas with a 1,1-dihydro-2,2-difluoro alcohol represented by formula (II):

        HOCH₂CF₂R_f   (II)

wherein R_f represents a perfluoroalkyl group or a fluoroalkyl group.

DETAILED DESCRIPTION OF THE INVENTION

[0015] The term "perfluoroalkyl group" as used herein means an alkyl group in which all the hydrogen atoms have been substituted by fluorine atoms. The term "fluoroalkyl group" as used herein means an alkyl group in which a part of the hydrogen atoms have been substituted by fluorine atoms.

[0016] By the method according to the present invention, a fluorine-containing olefin involving a 1,1-dihydro-2-fluorovinyl group can be produced cheaply by a simple procedure, i.e., a single-step reaction, with less amounts of wastes.

[0017] As a preferred embodiment of the method according to the present invention, a method in which a mixture of a fluoroalcohol and hydrogen gas is passed in a gaseous state through a reaction tube wihch is maintained at a high temperature is practically preferred. The reaction tube used in this embodiment is not limited in form, material, etc., and may be a conventional tubular reaction tube in which the interior of the tube can be maintaind at a desired temperature by heating from the outside, as described e.g., in JP-B-47-26484 and JP-A-60-185734. (The term "JP-B" as used herein means an "examined Japanese patent publication", and the term "JP-A" as used herein means an "unexamined published Japanese patent application") The material for forming the reaction tube may be stainless steel in the case of the use for a relatively short period, but is preferably Hastelloy, Inconel, etc. which are excellent in corrosion resistance.

[0018] A filler filled in the reaction tube may be used in the present invention. Examples of the filler include activated carbon, silica gel, alumina, zinc oxide, acid clay and potassium fluoride. The filler is preferably activated carbon in view of the selectivity of the objective product to by-products, e.g., HCF₂R_f, CH₃CF₂R_f and CH₂=CF₂. The activated carbon may be activated with zinc chloride or the like The activated carbon which can be used as the filler is described specifically, e.g., in Genso-betsu Shokubai Binran (Shokubai Kagaku Koza Vol. 10) (Manual of Catalysts by Elements (Lectures on Catalysts Vol. 10)), published on 1967 (Chijin Shokan, Japan).

[0019] When the molar ratio of hydrogen gas to the fluoroalcohol is increased, the selectivity of the final product tends to increase. If the ratio of hydrogen gas is too small, the amount of the decomposition products of the fluoroalcohol increases. Thus, the molar ratio of hydrogen gas to the fluoroalcohol is preferably 1 or more, more preferably from 2 to 7, and most preferably from 3 to 5.

[0020] The reaction temperature of the present invention is preferably from 350 to 700°C, and more preferably from 400 to 650°C. If the reaction temperature is too low, the reaction cannot be sufficiently proceeded. If the reaction temperature is too high, undesirable decomposition reactions tend to occur.

[0021] The fluoroalcohol used in the present inventoin is a 1,1-dihydro-2,2-difluoro alcohol that has a vapor pressure at the above reaction temperature represented by formula (II):

        HOCH₂CF₂R_f   (II)

wherein R_f represents a perfluoroalkyl group or a fluoroalkyl group. Examples of the 1,1-dihydro-2,2-difluoro alcohol include the fluoroalcohol represented by formula (IIa):

        XC_nF_2nCH₂OH   (IIa)

wherein X represents a hydrogen atom or a fluorine atom and n represents an integer of from 2 to 12, and preferably X represents a hydrogen atom and n represents 1, 3 or 5.

[0022] Therefore, examples of the fluorine-containing olefin involving a 1,1-dihydro-2-fluorovinyl group corresponding the above examples of fluoroalcohol include a compound represented by formula (Ia):

        XC_n-1F_2(n-1)CF = CH₂   (Ia)

wherein X represents a hydrogen atom or a fluorine atom, and n represents an integer of from 2 to 12.

[0023] The reaction scheme of the present invention is indicated below.

[0024] Other conditions such as the pressure and the contacting time of the reaction of the present invention are not particluarly limited, but the pressure of the reaction pressure is generally from 0.5 to 5 kg/cm², and the contacting time of the reaction is generally from 0.1 to 120 seconds. Preferably, the reaction pressure is from 0.5 to 1.5 kg/cm², and the contacting time of the reaction is from 1 to 10 seconds.

[0025] The objective product of the present invention can be isolated by known methods such as distillation after removing hydrogen fluoride by washing with water and drying with CaCl₂ or Molecular Sieves (a trade name of Linde Co.).

[0026] The present invention is described in more detail by referring to the following examples but the present invention is not construed as being limited thereto.

EXAMPLE 1

[0027] A tube made of stainless steel (SUS-316) having an inner diameter of 15.25 mm and a length of 650 mm as a reaction tube was placed in a longitudial tubular electric furnace of which temperature was controllable having a length of 600 mm so as to fablicate a reaction device.

[0028] After granular activated carbon (specific surface area: 800 to 1,200 m²/g, activated by zinc chloride) was filled in the reaction tube, the temperature of the interior of the reaction tube was maintained at 500°C. A mixed gas of 1,1,5-trihydro-2,2,3,3,4,4,5,5-octafluoropentanol (HOCH₂CF₂CF₂CF₂CF₂H) and hydrogen gas of which molar ratio is 1/3 was introduced into the reaction tube from the upper side such that the contacting time was 4 seconds and the reaction pressure was atmospheric pressure.

[0029] After 1 hour from the start of the reaction, gas exhausted from the lower side of the reaction tube was analyzed by a gas chromatography. As a result, 1,1,5-trihydro-2,3,3,4,4,5,5-heptafluoropentene-1 (CH₂=CFCF₂CF₂CF₂H) was obtained while the conversion ratio of the starting fluoroalcohol was 64% and the selectivity in the reaction product was 82%.

EXAMPLES 2 to 5

[0030] The same procedures as in Example 1 were repeated except that the starting fluoroalcohol, the filler in the reaction tube, the rection temeprature, the molar ratio of the fluoroalcohol and hydrogen, and the contacting time were varied as shown in Table 1 below. The results obtained are shown in Table 1 with the results of Example 1.

[0031] It is clear from the results shown in Table 1 that a fluorine-containing olefin involving a 1,1-dihydro-2-fluorovinyl group can be produced cheaply by a simple procedure, i.e., a single-step reaction, with less amounts of wastes in accordance with the present invention.

[0032] While the invention has been described in detail and with reference to specific examples thereof, it will be apparent to one skilled in the art that various changes and modifications can be made therein without departing from the spirit and scope thereof.

Claims

1. A method for producing a fluorine-containing olefin represented by formula (I):

        CH₂ = CFR_f   (I)

wherein R_f represents a perfluoroalkyl group or a fluoroalkyl group
   comprising the step of contacting, at a high temperature, hydrogen gas with a 1,1-dihydro-2,2-difluoro alcohol represented by formula (II):

        HOCH₂CF₂R_f   (II)

wherein R_f represents a perfluoroalkyl group or a fluoroalkyl group.

2. A method as claimed in claim 1, comprising the step of
   passing a mixed gas comprising said 1,1-dihydro-2,2-difluoro alcohol and hydrogen gas in which the molar ratio of hydrogen gas to said 1,1-dihydro-2,2-difluoro alcohol is 1 or more
   through a reacting tube at a temperature of from 350 to 700°C.

3. A method as claimed in claim 2, wherein the molar ratio of hydrogen gas to said 1,1-dihydro-2,2-difluoro alcohol is from 2 to 7.

4. A method as claimed in claim 3, wherein the molar ratio of hydrogen gas to said 1,1-dihydro-2,2-difluoro alcohol is from 3 to 5.

5. A method as claimed in claim 2, wherein said reaction temeprature is from 400 to 650°C.

6. A method as claimed in claim 2, wherein the pressure of said reaction is from 0.5 to 5 kg/cm².

7. A method as claimed in claim 6, wherein the pressure of said reaction is from 0.5 to 1.5 kg/cm².

8. A method as claimed in claim 2, wherein the contacting time of said reaction is from 0.1 to 120 seconds.

9. A method as claimed in claim 8, wherein the contacting time of said reaction is from 1 to 10 seconds.

Ansprüche

1. Verfahren zur Herstellung eines fluorhaltigen Olefins, dargestellt durch die Formel (I):

        CH₂ = CFR_f   (I)

worin R_f eine Perfluoralkylgruppe oder eine Fluoralkylgruppe bedeutet,
   bei dem bei einer hohen Temperatur Wasserstoffgas mit einem 1,1-Dihydro-2,2-difluoralkohol, dargestellt durch die Formel (II):

        HOCH₂CF₂R_f   (II)

worin R_f eine Perfluoralkylgruppe oder eine Fluoralkylgruppe bedeutet, in Berührung gebracht wird.

2. Verfahren nach Anspruch 1,
   bei dem ein gemischtes Gas, umfassend den 1,1-Dihydro-2,2-difluoralkohol und Wasserstoffgas, worin das Molverhältnis von Wasserstoffgas zu dem 1,1-Dihydro-2,2-difluoralkohol 1 oder mehr beträgt,
   durch ein Reaktionsrohr bei einer Temperatur von 350 bis 700°C geleitet.

3. Verfahren nach Anspruch 2, worin das Molverhältnis von Wasserstoffgas zu dem 1,1-Dihydro-2,2-difluoralkohol 2 bis 7 beträgt.

4. Verfahren nach Anspruch 3, worin das Molverhältnis von Wasserstoffgas zu dem 1,1-Dihydro-2,2-difluoralkohol 3 bis 5 beträgt.

5. Verfahren nach Anspruch 2, worin die Reaktionstemperatur 400 bis 650°C beträgt.

6. Verfahren nach Anspruch 2, worin der Reaktionsdruck 0,5 bis 5 kg/cm² beträgt.

7. Verfahren nach Anspruch 6, worin der Reaktionsdruck 0,5 bis 1,5 kg/cm² beträgt.

8. Verfahren nach Anspruch 2, worin die Berührungszeit der Reaktion 0,1 bis 120 Sekunden beträgt.

9. Verfahren nach Anspruch 8, worin die Berührungszeit der Reaktion 1 bis 10 Sekunden beträgt.

Revendications

1. Un procédé pour produire une oléfine fluorée représentée par la formule :

        CH₂ = CFR_f   (I)

dans laquelle R_f représente un groupe perfluoroalkyle ou un groupe fluoroalkyle,
   caractérisé en ce que l'on met en contact à température élevée du gaz hydrogène avec un 1,1-dihydro-2,2-difluoro-alcool représenté par la formule (II) :

        HOCH₂CF₂R_f   (II)

dans laquelle R_f représente un groupe perfluoroalkyle ou un groupe fluoroalkyle.

2. Un procédé selon la revendication 1,
   caractérisé en ce que l'on fait passer un mélange gazeux comprenant ledit 1,1-dihydro-2,2-difluoro-aLcool et le gaz hydrogène dans un rapport molaire du gaz hydrogène audit 1,1-dihydro-2,2-difluoro-alcool de 1 ou plus
   à travers un tube de réaction à une température de 350 à 700°C.

3. Un procédé selon la revendication 2, caractérisé en ce que le rapport molaire du gaz hydrogène audit 1,1-dihydro-2,2-difluoro-alcool est de 2 à 7.

4. Un procédé selon la revendication 3, caractérisé en ce que le rapport molaire du gaz hydrogène audit 1,1-dihydro-2,2-difluoro-alcool est de 3 à 5.

5. Un procédé selon la revendication 2, caractérisé en ce que la température de réaction est de 400 à 650°C.

6. Un procédé selon la revendication 2, caractérisé en ce que la pression de ladite réaction est de 0,5 à 5 bar.

7. Un procédé selon la revendication 6, caractérisé en ce que la pression de ladite réaction est de 0,5 à 1,5 bar.

8. Un procédé selon la revendication 2, caractérisé en ce que la durée de contact de ladite réaction est de 0,1 à 120 s.

9. Un procédé selon la revendication 8, caractérisé en ce que la durée de contact de ladite réaction est de 1 à 10 s.